Apparatus for making coupler dispersions

ABSTRACT

A method and apparatus relate to mixing solutions in which a well-stirred coupler/coupler solvent mixture is fed through a tube to an annular, flow-restriction plate arranged within an aqueous gelatin bulk mixture. A rotatable impeller is mounted in spaced relation to the plate and pumps the gelatin bulk mixture through the central opening or aperture in the plate and into the gap between the plate and the impeller. The impeller is provided with a number of concentric recesses interconnected by radial slots forming a circuitous path to the peripheral edge thereof. The flows of coupler/coupler solvent and gelatin bulk mixture are broken up by the radial slots and the annular recesses in conjunction with the fluid shear developed at the peripheral edge of the impeller.

United States Patent 1 Johnson et al.

[ Nov. 20, 1973 APPARATUS FOR MAKING COUPLER DISPERSIONS [75 Inventors: Benjamin Allen Johnson; Stephen L.

Royal; Robert A. Ackerman, all of Rochester, NY.

[73 Assignee: Eastman Kodak Company,

Rochester, NY.

22 Filed: July 28,197]

21 Appl. No.: 166,897

[52] US. Cl. 259/22, 259/96 [51] Int. Cl. B0lf 5/12, B01f 7/10 [58] Field of Search 259/7, 8, ll, 18, 259/22, 23, 24, 96; 261/93 [56] References Cited UNITED STATES PATENTS 3,233,876 2/1966 Faure et al 259/96 3,387,832 6/1968 Nelson 261/93 3,425,835 2/1969 Johnson et al... 259/23 X 3,570,818 3/1971 Johnson et a1... 259/22 2,996,287 8/1961 Audran 259/11 Primary Examiner-Harvey C. Homsby Assistant Examiner-Alan I. Cantor Att0rneyRobert W. Hampton et al.

[ 5 7 ABSTRACT A method and apparatus relate to mixing solutions in which a well-stirred coupler/coupler solvent mixture is fed through a tube to an annular, flow-restriction plate arranged within an aqueous gelatin bulk mixture. A

' rotatable impeller is mounted in spaced relation to the plate and pumps the gelatin bulk mixture through the central opening or aperture in the plate and into the gap between the plate and the impeller. The impeller is provided with a number of concentric recesses interconnected by radial slots forming a circuitous path to the peripheral edge thereof. The flows of coupler/- coupler solvent and gelatin bulk mixture are broken up by the radial slots and the annular recesses in conjunction with the fluid shear developed at the peripheral edge of the impeller.

4 Claims, 4 Drawing Figures PATENTED NOV 2 0 I975 F/GZ INVENTOR.

M 5 N W J A N M m B STEPHEN L. ROYAL ROBERT 14.4CKERMA/V AGE/VT APPARATUS FOR MAKING COUPLER DISPERSIONS FIELD OF THE INVENTION This invention relates to apparatus for the preparation of coupler dispersions and, more particularly to apparatus for preparing coupler dispersions which are crystal-free and have particle sizes of 1 micron or less.

DESCRIPTION OF THE PRIOR ART In the photographic art the addition of respective reagents or addenda to an aqueous gelatin solution is usually accomplished by the agitation provided by a simple, propeller-type impeller. The actual dispersion is accomplished by passing the mixture, after the addenda has been added, through a colloid mill, homogenizer, or the like; and the dispersions can be stabilized by the addition of emulsifying agents, such as those of the well-known higher fatty, alcohol sulfate type.

With the addition of one or more such addenda compositions to a gelatin solution, the addition obtained results in areas of the gelatin solution having a local, high concentration of the solution which results in coagulated particles. These coagulated particles interfere with filtration of the gelatin solution and also increase the occurrence of defects in the coatings which result therefrom.

Normally, coupler dispersions for use in photographic silver halide emulsions can be prepared by mixing a coupler with a low boiling hydrophobic organic solvent, for example, ethylacetate, dispersing the mixture by passing it through a colloid mixer several times, cooling the mixture until gelled, shredding the gelled dispersion, then washing the shreds with water and drying the shreds to remove the low boiling organic solvent. At the same time, a low molecular weight, organic crystalloidal material, for example, di-n-butylphthalate, is dispersed in gelatin by passing the mixture through a colloid mill several times and filtering the dispersion through a silk screen to remove air bubbles. The two dispersions are then mixed, heated by a water bath at 40C for several minutes, and then added to a photographic emulsion. Such a procedure is described in U.S. Pat. No. 2,801,170. A somewhat similar technique is disclosed in U. S. Pat. No. 2,801,171 for the preparation of dispersions having a low coupler to solvent ratio. In both of these patents, colloid mills are relied upon to provide a small particle size dispersion.

The prior art also discloses other means for obtaining coupler dispersions of small particle size, for example, a blender, an ultrasonic wave generator in the aqueous gelatin solution, electrostatic atomization, and more sophisticated liquid mixing apparatus which can be used for dispersing coupler/solvent mixtures in aqueous gelatin solutions. In the prior art there is no indication of the size of the coupler particles in the dispersion other than when the two solutions are mixed using the apparatus of the present invention, the fine dispersion of color coupler is improved, since the size of the coupler particles is considerably more uniform."

As shown by the prior art, a ballasted nonhydrophilic coupler in a solvent, usually an ester, can be dissolved and dispersed mechanically by means of a homogenizer or colloid mill in gelatin in the presence of a surface-active agent. Such dispersions are then incorporated in a photographic emulsion, and a desired particle size is 1 micron or less. It is important to prevent the coupler from undergoing crystallization upon prolonged storage; and, frequently, the mixture must be passed through a homogenizer or colloid mill several times in order to obtain the desired particle size of less than 1 micron. The particle size of the coupler dispersion can effect the microscopic structure of the dye image being formed. The degree of dispersity of the dye deposit influences the absorption of the dye and the graininess and, possibly, definition of the dye image can be effected by the morphology of the dye deposit. Dyes can be formed only to the extent'to which the coupler has been supplied per unit of space. Consequently, a uniform coupler dispersion having submicroscopic, that is, less than 1 micron particles would be highly desirable.

For manufacturing purposes, it would also be desirable to prepare large batches of submicroscopic unifonn coupler dispersions. Obviously, blenders and other types of mixing devices do not readily lend themselves as a suitable homogenizer for such large batches of coupler dispersions. In addition, in order to obtain a coupler dispersion having the desired particle size, the dispersion must be recycled several times through a colloid mill. As a result, the use of colloid mills is very time-consuming and not particularly satisfactory for preparing a large batch of coupler dispersion.

SUMMARY OF THE INVENTION One object of the invention is to provide apparatus by which a uniform and crystal-free dispersion can be prepared.

Another object of the invention is to provide apparatus by which a coupler/coupler solvent can be uniformly mixed with an aqueous gelatin solution to provide a uniform nd crystal-free dispersion.

Yet another object of the invention is to provide apparatus by which a uniform and crystal-free dispersion can be prepared without producing any adverse sensitometric effects relative to the final emulsion with which the dispersion is used.

A still further object of the invention is to provide apparatus for preparing a coupler dispersion in which the resultant particle size in the dispersion is of the order of about 1 micron.

These and other objects and advantages of the invention will be apparent from the description which follows.

The above objects of the invention are attained by apparatus in which a well-stirred coupler/coupler solvent mixture is fed through a tube to an annular, flowrestriction plate arranged within an aqueous gelatin bulk mixture. A rotatable impeller is mounted in spaced relation to the plate and pumps the gelatin bulk mixture through the central opening or aperture in the plate and into the gap between the plate and the impeller. The impeller is provided with a number of concentric recesses interconnected by radial slots forming a circuitous path to the peripheral edge thereof. The coupler/coupler solvent flows into the gap and the innermost recess and is completely surrounded by the flow of gelatin bulk mixture that is moved through the central opening by the impeller. The centrifugal force generated by the impeller causes the two flows to be mixed upon movement thereof through the radial slots and the adjacent recesses to the peripheral edge of the impeller where the mixture is expelled into the gelatin bulk mixture. The flows of coupler/coupler solvent and gelatin bulk mixture are broken up by the radial slots and the annular recesses in conjunction with the fluid shear developed at the peripheral edge of the impeller.

DESCRIPTION OF THE DRAWING Reference is now made to the accompanying drawings wherein like reference numerals designate like parts and wherein:

FIG. 1 is a vertical sectional view through apparatus embodying the invention;

FIG. 2 is a vertical sectional view showing in more detail the relation of the impeller and the annular, flowrestriction plate;

FIG. 3 is an elevational view of the impeller showing the concentric impeller recesses and the radial slots interconnecting said recesses; and

FIG. 4 is an elevational view of the annular flowrestriction plate showing the central opening and the feed tube for introducing the coupler/coupler solvent liquid.

DESCRIPTION OF THE PREFERRED EMBODIMENT Reference is now made to FIG. 1 in which the coupier/coupler solvent liquid is disclosed as being contained within a receptacle 11 that can be heated by means of a unit contained within the jacket 12 to maintain the solvent at the proper temperature. An aqueous gelatin solution 13 is contained in a tank 14, which is provided with a jacket 15 containing heating means for maintaining the gelatin solution at the proper temperature. While the liquid 10 and solution 13 have just been described as a coupler/coupler solvent liquid and an aqueous gelatin solution, in a broader sense, the first 10) can be referred to as a dispersed phase liquid, whereas, the latter (13) can be defined as a continuous phase dispersion medium. This terminology is noted to be sure it is understood that the method and apparatus about to be described in more detail for the preparation of a coupler dispersion for use in a photographic emulsion can also be used with equivalent results for mixing any liquids that can be defined by the broader definitions.

A fixed plate member is provided with an annular opening 21 and has generally planar surfaces 22 and 23. The plate 20 is, preferably, circular in shape with a concentric, circular opening 21, thereby providing an annular shape. A feed tube 24 is connected at one end to the receptacle 11 and is fixedly mounted within tank 14 in a manner not shown. The other end of tube 24 supports plate member 20 by means of straps 25 so tube 24 is generally central with respect to opening 21.

A rotatable impeller member is circular in shape and is secured or fixed by pin 31 to the end of a shaft 32 that is driven by motor 33. These elements are supported by bracket 34 mounted on tank 14 so that impeller is in the gelatin solution 13. The impeller member 30 has a planar surface 35 and is provided with at least two concentric, annular recesses 36 and 37. The recesses open to surface 35, as shown in FIG. 2, and the land 38 between recesses 36 and 37, and the land 39 between recess 37 and the peripheral edge40 are inter connected by a number of radial slots 41 and 42, respectively. The impeller member 30 is immersed in the gelatin solution 13, as shown in FIG. 1, and is arranged with the surface 35 in close proximity to the surface 22 of plate 20, thereby forming a gap of less than 0.25

inches therebetween. By means of bracket 34 and suitable means (not shown) for mounting the tube 24, the plate 20 and impeller member 30 are maintained in a fixed, spaced relation'within tank 14 so the impeller 30 can be rotated in the gelatin solution 13. edge 40, and into the gelatin solution 13. The impeller 30 is designed to provide arate of about 10,000rpminches (diameter X rpm). Also, the number andcross section of slots 41 and 42 are chosen so as to create asuction or vacuum at tube 24 that is at least3O inches water.

The recesses 36 and 37 with slots 41 and 42 provide a type of circuitous path through which the liquid 10 and solution 13 are moved and mixed and finally expelled at the peripheral edge ofmember 30. The circuitous path can take other forms and can be provided relative to the surface 22 of member 20 or in both of members 20 and 30. It is believed that a more uniform and finer dispersion can be obtained if such a path is provided in both of members 20 and 30.

With the introduction of the coupler/coupler solvent liquid, the vacuum or suction developed by impeller 30 draws the liquid into gap 45 and the innermost recesses 36. It will be noted that with respect to FIGS. 2 and 4, that the flow of gelatin solution through opening 21 completely surrounds the flow of the coupler/coupler solvent liquid via tube 24. As the two flows of liquid enter recess 36, they are broken up and thoroughly intermixed by the radial slots 41 and 42, the annular recesses 36 and 37, and the fluid shear produced at the peripheral edge 40 of the impeller 30. With this action, the two flows are thoroughly mixed before being introduced into the gelatin bulk mixture 13 by the movement thereof through slots 41 and 42 and gap 45.

After a complete dispersion has been accomplished, a valve in a line 56 is opened connecting tank 14 to a pump 57 which moves the dispersion through a filter 58 and then into and through a heat exchanger 59. Upon discharge from the heat exchanger 59, the dispersion can be treated and converted into a firm jelly or solid form for storage purposes.

The following example will serve to illustrate the invention, but is not to be considered as a limitation thereof.

The coupler/coupler solvent mixture and aqueous gelatin solution are made as follows:

Coupler/coupler solvent mixture N-(p-Benzoylacetamidobenzenesulfonyl)-N,-y-

Phenylpropyl-p-toluidine 4 Kg. tri-cresyl phosphates 2 Kg. 2-ethoxy ethylacetate 8 Kg. Temperature 137. 8C

Aqueous gelatin mixture Gelatin 2,994 Kg Distilled water 26.943 Kg Sodium Alkylnaphthalene sulfonate (Nekal BX-78, GAF Corporation) 2.994 Kg used, the volatile solvent can be removed by evaporation.

This technique permits a uniform and crystal-free dispersion to be prepared. The resultant particle size is of the order of one-half to one mircon. For a still further reduction in particle size, the dispersion can be passed through a colloid mill instead of a centrifugal pump prior to the filtration step.

This invention has been described in detail with particular reference to preferred embodiments thereof, but it will be understood that variations and modifications can be effected within the spirit and scope of the invention.

We claim:

1. A device for dispersing a dispersed phase liquid in a continuous phase, dispersion medium contained in a receptacle, comprising:

a fixed, plate member having a planar surface and an annular opening and immersed in said dispersion medium within said receptacle;

a rotatable member having a planar surface and a number of concentric annular recesses open to the planar surface of said plate member and interconnected one to the other to the peripheral edge thereof by a number of radial slots and arranged in said dispersion medium with the planar surface thereof in spaced, generally parallel relation to that of said plate member so as to form a narrow gap therebetween for introducing a flow of said dispersion medium through said opening into said gap and the innermost of said recesses; and

means connected to said plate member for introducing a flow of said phase liquid into said gap and the innermost of said recesses;

whereby said rotatable member mixes said flows during movement thereof from said innermost recess through the circuitous path formed by said radial slots, other recesses and said gap for expulsion into said dispersion medium at said peripheral edge.

2. A device in accordance with claim 1 wherein the planar surfaces of said plate member and said rotatable member are spaced apart less than 0.25 inches.

3. A device in accordance with claim 1 wherein said rotatable member creates a suction to draw said phase liquid into said gap and said innermost recess.

4. A device in accordance with claim 1 wherein said means for introducing the flow of said phase liquid is arranged generally centrally of said opening whereby the flow of said dispersion medium generally surrounds that of said phase liquid. 

1. A device for dispersing a dispersed phase liquid in a continuous phase, dispersion medium contained in a receptacle, comprising: a fixed, plate member having a planar surface and an annular opening and immersed in said dispersion medium within said receptacle; a rotatable member having a planar surface and a number of concentric annular recesses open to the planar surface of said plate member and interconnected one to the other to the peripheral edge thereof by a number of radial slots and arranged in said dispersion medium with the Planar surface thereof in spaced, generally parallel relation to that of said plate member so as to form a narrow gap therebetween for introducing a flow of said dispersion medium through said opening into said gap and the innermost of said recesses; and means connected to said plate member for introducing a flow of said phase liquid into said gap and the innermost of said recesses; whereby said rotatable member mixes said flows during movement thereof from said innermost recess through the circuitous path formed by said radial slots, other recesses and said gap for expulsion into said dispersion medium at said peripheral edge.
 2. A device in accordance with claim 1 wherein the planar surfaces of said plate member and said rotatable member are spaced apart less than 0.25 inches.
 3. A device in accordance with claim 1 wherein said rotatable member creates a suction to draw said phase liquid into said gap and said innermost recess.
 4. A device in accordance with claim 1 wherein said means for introducing the flow of said phase liquid is arranged generally centrally of said opening whereby the flow of said dispersion medium generally surrounds that of said phase liquid. 